US5599979A - Separation of formic acid from acetic acid by extractive distillation - Google Patents
Separation of formic acid from acetic acid by extractive distillation Download PDFInfo
- Publication number
- US5599979A US5599979A US08/524,670 US52467095A US5599979A US 5599979 A US5599979 A US 5599979A US 52467095 A US52467095 A US 52467095A US 5599979 A US5599979 A US 5599979A
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- US
- United States
- Prior art keywords
- acid
- acetic acid
- formic acid
- formic
- separation
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
- C07C51/44—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
Definitions
- This invention relates to a method for separating formic acid from acetic acid using certain organic compounds as the agent in extractive distillation.
- Extractive distillation is the method of separating close boiling compounds from each other by carrying out the distillation in a multiplate rectification column in the presence of an added liquid or liquid mixture, said liquid(s) having a boiling point higher than the compounds being separated.
- the extractive agent is introduced near the top of the column and flows downward until it reaches the stillpot or reboiler. Its presence on each plate of the rectification column alters the relative volatility of the close boiling compounds in a direction to make the separation on each plate greater and thus require either fewer plates to effect the same separation or make possible a greater degree of separation with the same number of plates.
- the extractive agent should boil higher than any of the close boiling liquids being separated and not form minimum azeotropes with them.
- the extractive agent is introduced a few plates from the top of the column to insure that none of the extractive agent is carried over with the lowest boiling component. This usually requires that the extractive agent boil about twenty Celcius degrees or more higher than the lowest boiling component.
- the object of this invention is to provide a process or method of extractive distillation that will enhance the relative volatility of formic acid to acetic acid in their separation in a rectification column. It is a further object of this invention to identify certain organic compounds that are stable, are effective as extractive distillation agents and can be readily separated from formic acid or acetic acid and recycled to the extractive distillation column with little decomposition.
- the objects of this invention are provided-by a process for the separation of formic acid from acetic acid which entails the use of certain organic compounds when-separately employed as the agent in extractive distillation.
- Example 1 Thirty grams Of formic acid, 40 grams of acetic acid and 30 grams of 2-ethyl hexanoic acid were charged to a vapor-liquid equilibrium still and refluxed for three hours. Analysis indicated a vapor composition of 50.7% formic acid, 49.3% acetic acid; a liquid composition of 40.1% formic acid, 59.9% acetic acid. This is a relative volatility of formic acid to acetic acid of 1.55.
- Example 2 Thirty-five grams of formic acid, 15 grams of acetic acid and 50 grams of propionic acid were charged to a vapor-liquid equilibrium still and refluxed for six hours. Analysis indicated a vapor composition of 32.6% formic acid, 32.0% acetic acid and 35.4% propionic acid; a liquid composition of 20.3% formic acid, 28.8% acetic acid and 50.9% propionic acid. This is a relative volatility of formic acid to acetic acid of 1.45; of formic acid to propionic acid of 2.3 and of acetic acid to propionic acid of 1.6.
Abstract
Formic acid is difficult to separate from acetic acid by conventional distillation or rectification because of the close proximity of their boiling points. Formic acid can be readily separated from acetic acid by using extractive distillation. Effective agents are propionic acid, butyric acid, valeric acid and 2-ethyl hexanoic acid.
Description
This invention relates to a method for separating formic acid from acetic acid using certain organic compounds as the agent in extractive distillation.
Extractive distillation is the method of separating close boiling compounds from each other by carrying out the distillation in a multiplate rectification column in the presence of an added liquid or liquid mixture, said liquid(s) having a boiling point higher than the compounds being separated. The extractive agent is introduced near the top of the column and flows downward until it reaches the stillpot or reboiler. Its presence on each plate of the rectification column alters the relative volatility of the close boiling compounds in a direction to make the separation on each plate greater and thus require either fewer plates to effect the same separation or make possible a greater degree of separation with the same number of plates. The extractive agent should boil higher than any of the close boiling liquids being separated and not form minimum azeotropes with them. Usually the extractive agent is introduced a few plates from the top of the column to insure that none of the extractive agent is carried over with the lowest boiling component. This usually requires that the extractive agent boil about twenty Celcius degrees or more higher than the lowest boiling component.
At the bottom of a continuous column, the less volatile components of the close boiling mixtures and the extractive agent are continuously removed from the column. The usual methods of separation of these two components are the use of another rectification column, cooling and phase separation, or solvent extraction.
Formic acid, B.P.=101° C. and acetic acid, B.P.=118° C. have a relative volatility of 1.23 and are difficult to separate by conventional rectification. Table 1 shows that to get 99% purity, sixty actual plates are required. For an agent giving a relative volatility of 1.55, only twenty-eight actual plates are required. An improvement of this magnitude represents a clear economic and operational advantage to the separation of these industrially important chemicals.
TABLE 1
______________________________________
Theoretical and Actual Plates Required vs. Relative
Volatility for Formic Acid-Acetic Acid Separation
Relative
Theoretical Plates Required
Actual Plates
Volatility
At Total Reflux, 99% Purity
Required, 75% Eff.
______________________________________
1.23 45 60
1.50 23 31
1.55 21 28
______________________________________
The object of this invention is to provide a process or method of extractive distillation that will enhance the relative volatility of formic acid to acetic acid in their separation in a rectification column. It is a further object of this invention to identify certain organic compounds that are stable, are effective as extractive distillation agents and can be readily separated from formic acid or acetic acid and recycled to the extractive distillation column with little decomposition.
The objects of this invention are provided-by a process for the separation of formic acid from acetic acid which entails the use of certain organic compounds when-separately employed as the agent in extractive distillation.
TABLE 2
______________________________________
Effective Extractive Distillation Agents For
Separating Formic Acid From Acetic Acid
Compounds Relative Volatility
______________________________________
None 1.23
Butyric acid 1.65
Valeric acid 1.50
2-Ethyl hexanoic acid
1.55
Propionic acid 1.45
Propionic acid-Acetic acid
1.60
______________________________________
I have discovered that certain organic compounds will effectively increase the relative volatility between formic acid and acetic acid during rectification when employed as the agent in extractive distillation. Table 2 summarizes the data obtained with these agents. The agents which are effective are propionic acid, butyric acid, valeric acid and 2-ethyl hexanoic acid.
The usefulness or utility of this invention can be demonstrated by referring to the data presented in Tables 1 and 2. All of the successful agents show that formic acid can be separated from acetic acid by means of extractive distillation in a rectification column and that the ease of separation as measured by relative volatility is considerable
Example 1: Thirty grams Of formic acid, 40 grams of acetic acid and 30 grams of 2-ethyl hexanoic acid were charged to a vapor-liquid equilibrium still and refluxed for three hours. Analysis indicated a vapor composition of 50.7% formic acid, 49.3% acetic acid; a liquid composition of 40.1% formic acid, 59.9% acetic acid. This is a relative volatility of formic acid to acetic acid of 1.55.
Example 2: Thirty-five grams of formic acid, 15 grams of acetic acid and 50 grams of propionic acid were charged to a vapor-liquid equilibrium still and refluxed for six hours. Analysis indicated a vapor composition of 32.6% formic acid, 32.0% acetic acid and 35.4% propionic acid; a liquid composition of 20.3% formic acid, 28.8% acetic acid and 50.9% propionic acid. This is a relative volatility of formic acid to acetic acid of 1.45; of formic acid to propionic acid of 2.3 and of acetic acid to propionic acid of 1.6.
Claims (2)
1. A method for recovering formic acid from a mixture of formic acid and acetic acid which comprises distilling a mixture of formic acid and acetic acid in a rectification column in the presence of about one part by weight of an extractive agent per part of formic acid-acetic acid mixture, recovering the formic acid as overhead product and obtaining the acetic acid and the extractive agent from the stillpot, wherein said extractive agent consists of one material selected from the group consisting of propionic acid, butyric acid, valeric acid and 2-ethyl hexanoic acid.
2. A method for recovering propionic acid from a mixture of propionic acid, formic acid and acetic acid which comprises distilling a mixture of propionic acid, formic acid and acetic acid in a rectification column, recovering the formic acid and the acetic acid as overhead product and obtaining the propionic acid from the stillpot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/524,670 US5599979A (en) | 1995-09-08 | 1995-09-08 | Separation of formic acid from acetic acid by extractive distillation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/524,670 US5599979A (en) | 1995-09-08 | 1995-09-08 | Separation of formic acid from acetic acid by extractive distillation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US5599979A true US5599979A (en) | 1997-02-04 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US08/524,670 Expired - Fee Related US5599979A (en) | 1995-09-08 | 1995-09-08 | Separation of formic acid from acetic acid by extractive distillation |
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| Country | Link |
|---|---|
| US (1) | US5599979A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5868908A (en) * | 1997-09-09 | 1999-02-09 | Wrr Environmental Services Co., Inc. | Separation of inorganic salts from dimethyl sulfoxide |
| US20060059769A1 (en) * | 2004-09-21 | 2006-03-23 | The Board Of Trustees Of The University Of Illinois | Low contaminant formic acid fuel for direct liquid fuel cell |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1813636A (en) * | 1928-02-07 | 1931-07-07 | Ig Farbenindustrie Ag | Process of separating formic acid from acetic acid |
| US4692219A (en) * | 1986-12-03 | 1987-09-08 | Celanese Chemical Co. | Separation of formic acid from acetic acid by extractive distillation |
-
1995
- 1995-09-08 US US08/524,670 patent/US5599979A/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1813636A (en) * | 1928-02-07 | 1931-07-07 | Ig Farbenindustrie Ag | Process of separating formic acid from acetic acid |
| US4692219A (en) * | 1986-12-03 | 1987-09-08 | Celanese Chemical Co. | Separation of formic acid from acetic acid by extractive distillation |
Non-Patent Citations (2)
| Title |
|---|
| E. Lloyd Jones, "Economc Saving. . . Solvent Extraction", Chemistry and Industry, pp. 1590-1592. |
| E. Lloyd Jones, Economc Saving. . . Solvent Extraction , Chemistry and Industry, pp. 1590 1592. * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5868908A (en) * | 1997-09-09 | 1999-02-09 | Wrr Environmental Services Co., Inc. | Separation of inorganic salts from dimethyl sulfoxide |
| US20060059769A1 (en) * | 2004-09-21 | 2006-03-23 | The Board Of Trustees Of The University Of Illinois | Low contaminant formic acid fuel for direct liquid fuel cell |
| US7618725B2 (en) | 2004-09-21 | 2009-11-17 | The Board Of Trustees Of The University Of Illinois | Low contaminant formic acid fuel for direct liquid fuel cell |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| REMI | Maintenance fee reminder mailed | ||
| LAPS | Lapse for failure to pay maintenance fees | ||
| FP | Lapsed due to failure to pay maintenance fee |
Effective date: 20010204 |
|
| STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |